EP4092813A1 - Échangeur de chaleur de refroidissement - Google Patents

Échangeur de chaleur de refroidissement Download PDF

Info

Publication number
EP4092813A1
EP4092813A1 EP21741235.2A EP21741235A EP4092813A1 EP 4092813 A1 EP4092813 A1 EP 4092813A1 EP 21741235 A EP21741235 A EP 21741235A EP 4092813 A1 EP4092813 A1 EP 4092813A1
Authority
EP
European Patent Office
Prior art keywords
refrigerants
header
tube
heat exchanger
flow
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
EP21741235.2A
Other languages
German (de)
English (en)
Inventor
Kazuya KURAHASHI
Mingdi WANG
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Valeo Japan Co Ltd
Original Assignee
Valeo Japan Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Valeo Japan Co Ltd filed Critical Valeo Japan Co Ltd
Publication of EP4092813A1 publication Critical patent/EP4092813A1/fr
Pending legal-status Critical Current

Links

Images

Classifications

    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/60—Heating or cooling; Temperature control
    • H01M10/61—Types of temperature control
    • H01M10/613—Cooling or keeping cold
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/60—Heating or cooling; Temperature control
    • H01M10/62—Heating or cooling; Temperature control specially adapted for specific applications
    • H01M10/625—Vehicles
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/60—Heating or cooling; Temperature control
    • H01M10/64—Heating or cooling; Temperature control characterised by the shape of the cells
    • H01M10/647—Prismatic or flat cells, e.g. pouch cells
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/60—Heating or cooling; Temperature control
    • H01M10/65—Means for temperature control structurally associated with the cells
    • H01M10/655—Solid structures for heat exchange or heat conduction
    • H01M10/6556—Solid parts with flow channel passages or pipes for heat exchange
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/60—Heating or cooling; Temperature control
    • H01M10/65—Means for temperature control structurally associated with the cells
    • H01M10/656—Means for temperature control structurally associated with the cells characterised by the type of heat-exchange fluid

Definitions

  • the present invention relates to a cooling heat exchanger for cooling high-temperature battery cells mounted in a vehicle.
  • Patent Literature 1 discloses a refrigerant type cooling heat exchanger for cooling a battery.
  • the cooling heat exchanger of Patent Literature 1 includes a plurality of flat tubes (refrigerant pipes) provided between two headers (manifolds) and coming in contact with the battery.
  • the headers are disposed to extend in a vertical direction and the tubes are thermally coupled with a side surface of the battery. That is, the tubes come in contact with the side surface of the battery to enable heat exchange.
  • refrigerants flowing in relatively upstream-side tubes in a refrigerant flow passage formed by the headers and the tubes are in a gas-liquid mixture state of sufficiently containing a liquid and have a sufficient battery cooling capacity.
  • the refrigerants are heated by the heat of the battery when flowing in the tubes, whereby the refrigerants in a liquid state evaporate and decrease and a ratio of refrigerants in a gas state increases.
  • a battery module of Patent Literature 2 includes a plurality of batteries disposed in a battery pack case.
  • the batteries are stacked in the vertical direction and a transverse direction and form groups, so that a plurality of groups are disposed in one battery pack case.
  • the cooling heat exchanger is configured with three or more headers and an intermediate header is disposed between the battery groups, whereby it is possible to reduce an unintended deformation of the tubes and to form thermally coupling of the tubes with the side surface of each battery group.
  • An object of the present invention is to reduce an increase in a ratio of gas-phase refrigerants and thereby keep uniformity of a battery temperature distribution in refrigerants flowing through upper tubes among a plurality of tubes disposed downstream of an intermediate header in a vertical direction in a battery cooling module including the intermediate header.
  • a cooling heat exchanger (30; 30A; 30B) through which refrigerants in a gas-liquid mixture state flow and that cools battery cells (21) for a vehicle, including:
  • the cooling heat exchanger (30; 30A, 30B) includes:
  • the embodiment it is possible to reduce an increase in a ratio of gas-phase refrigerants and thereby keep uniformity of a battery temperature distribution in refrigerants flowing through upper tubes among a plurality of tubes disposed downstream of an intermediate header in a vertical direction in a battery cooling module including the intermediate header.
  • Fig. 1 illustrates three battery stacked bodies 20 in which electric power is accumulated, a cooling heat exchanger 30 for cooling these battery stack bodies 20, and a battery pack case 10 that accommodates the battery stacked bodies 20 and the cooling heat exchanger 30.
  • the battery pack case 10, the battery stacked bodies 20, and the cooling heat exchanger 30 are mounted in, for example, an electric-powered vehicle that travels by driving a travel motor using electric power or a hybrid vehicle having a power source formed from an internal combustion engine and a motor.
  • the battery pack case 10 is mounted in the vehicle and formed from a metal or a resin. While Fig. 1 illustrates the battery pack case 10 as a container that accommodates the battery stacked bodies 20 and the cooling heat exchanger 30 inside and that has an open top surface, the battery pack case 10 is normally formed as a hermetic container such that certain airtightness can be ensured in the battery pack case 10. Ensuring the airtightness enables battery cells 21 that are precision products to be isolated and protected from dust, water, fat, and the like coming flying from an outside world.
  • Each of the battery stacked bodies 20 includes a plurality of stacked battery cells 21 and a soaking layer 22 disposed on a surface opposed to the cooling heat exchanger 30.
  • a stacking direction of the battery cells 21 is not limited to a vertical direction as illustrated in Fig. 1 and may be a transverse direction or a longitudinal direction (not illustrated).
  • Providing the soaking layer 22 enables a reduction in variation of a temperature distribution of each of the battery cells 21.
  • a high thermal conductivity material such as an aluminum alloy or a stainless steel alloy is used for the soaking layer 22.
  • the battery cells 21 have a function to accumulate electric power to be supplied to the motor for driving the vehicle (not illustrated), and generate heat and becomes hot when being charged.
  • the soaking layer 22 of each battery stacked body 20 transfers the heat of the hot battery cells 21, which is thermally coupled with the cooling heat exchanger 30 and which becomes hot, to the cooling heat exchanger 30.
  • the cooling heat exchanger 30 is coupled to a refrigeration cycle, not illustrated, and disposed, in particular, downstream of an expanding device.
  • refrigerants in a gas-liquid mixture state that serve as cooling heating mediums flow through the cooling heat exchanger 30.
  • refrigerants to be used include fluorocarbon refrigerants (HFC-134a, R-1234yf, and R-12).
  • the cooling heat exchanger 30 is formed from, for example, a high thermal conductivity material such as an aluminum alloy or a copper alloy.
  • the cooling heat exchanger 30 includes four headers H (an inlet header H1, intermediate headers H2 and H3, and an outlet header H4) each formed into a cylindrical shape and extending vertically, heat exchange tubes T (upper tubes Ta1, Ta2, and Ta3 and lower tubes Tb1, Tb2, and Tb3)that is supported by the headers H and in which the refrigerants flow, an inlet section 31 that is connected to an upper portion of the inlet header H1 and into which the refrigerants flow, and an outlet section 32 that is connected to a lower portion of the outlet header H4 and that discharges the refrigerants.
  • An interior of the intermediate header H2 is partitioned into an upper space 42a and a lower space 42b that is located below this upper space 42a by a partition member S2.
  • An interior of the intermediate header H3 is partitioned into an upper space 43a and a lower space 43b that is located below this upper space 43a by a partition member S3.
  • the inlet section 31 has a cylindrical flange portion provided in a metal tube and inserted into a hole portion formed in the inlet header H1. A downstream end of the inlet section 31 opens to an internal space 41 of the inlet header H1.
  • the outlet section 32 has a cylindrical flange portion provided in a metal tube and inserted into a hole portion formed in the outlet header H4. An upstream end of the outlet section 32 opens to an internal space 44 of the outlet header H4.
  • the heat exchange tubes T are flat cylindrical members and a plurality of walls can be formed in the heat exchange tubes T along a refrigerant flow direction (refer to Fig.5 ).
  • a manufacturing method such as extrusion, lamination of two tube plates, and reel forming of one tube plate is used.
  • the first upper tube Ta1 communicates the internal space 41 of the inlet header H1 with the upper space 42a of the intermediate header H2.
  • the first lower tube Tb1 communicates the internal space 41 of the inlet header H1 with the lower space 42b of the intermediate header H2.
  • the second upper tube Ta2 communicates the upper space 42a of the intermediate header H2 with the upper space 43a of the intermediate header H3.
  • the second lower tube Tb2 communicates the lower space 42b of the intermediate header H2 with the lower space 43b of the intermediate header H3.
  • the third upper tube Ta3 communicates the upper space 43a of the intermediate header H3 with the internal space 44 of the outlet header H4.
  • the third lower tube Tb3 communicates the lower space 43b of the intermediate header H3 with the internal space 44 of the outlet header H4.
  • the four headers H1, h2, H3, and H4 include the inlet header H1 in which the inlet section 31 is disposed, the intermediate header H2 that is disposed downstream of the inlet header H1 and with which the first upper tube Ta1 and the first lower tube Tb1 are coupled, the intermediate header H3 that is disposed downstream of the intermediate header H2 and with which the second upper tube Ta2 and the second lower tube Tb2 are coupled, and the outlet header H4 that is disposed downstream of the intermediate header H3 and with which the third upper tube Ta3 and the third lower tube Tb3 are coupled. While Figs. 1 to 3 illustrate that the four headers H1, H2, H3, and H4 are all equal in length dimensions, the present invention is not limited to this.
  • height dimensions of the headers H1, H2, H3, and H4 may be changed as appropriate.
  • vertical positions of the upper tubes Ta and the lower tubes Tb may be changed as appropriate.
  • the cooling heat exchanger 30 is preferably formed by integrally bonding the four headers H, the eight heat exchange tubes T, the inlet section 31, the outlet section 32, and the partition members S2 and S3 by brazing. High rigidity of the cooling heat exchanger 30 can be thereby ensured.
  • arrows indicate a flow direction and a flow volume of the refrigerants and black circles each indicate a liquid refrigerant.
  • Gas-liquid mixture refrigerants flowing through the inlet section 31 and flowing into the inlet header H1 branch off in the internal space 41 of the inlet header H1 generally vertically, and a part of the refrigerants flow into the first upper tube Ta1 while a rest thereof flow into the first lower tube Tb1.
  • the refrigerants flowing in the first upper tube Ta1 and the first lower tube Tb1 carry out heat exchange with the battery cells 21 via the soaking layers 21.
  • the refrigerants flowing out of the first upper tube Ta1 flow into the upper space 42a of the intermediate header H2.
  • the refrigerants flowing out of the first lower tube Tb1 flow into the lower space 42b of the intermediate header H2.
  • the gas-liquid mixture refrigerants flowing into the upper space 42a of the intermediate header H2 flow into the second upper tube Ta2.
  • the gas-liquid mixture refrigerants flowing into the lower space 42b of the intermediate header H2 flow into the second lower tube Tb2.
  • the refrigerants flowing in the second upper tube Ta2 and the second lower tube Tb2 carry out heat exchange with the battery cells 21 via the soaking layers 21.
  • the refrigerants flowing out of the second upper tube Ta2 flow into the upper space 43a of the intermediate header H3.
  • the refrigerants flowing out of the second lower tube Tb2 flow into the lower space 43b of the intermediate header H3.
  • the gas-liquid mixture refrigerants flowing into the upper space 43a of the intermediate header H3 flow into the third upper tube Ta3.
  • the gas-liquid mixture refrigerants flowing into the lower space 43b of the intermediate header H3 flow into the third lower tube Tb3.
  • the refrigerants flowing in the third upper tube Ta3 and the third lower tube Tb3 carry out heat exchange with the battery cells 21 via the soaking layers 21.
  • the refrigerants flowing out from the third upper tube Ta3 flow into the internal space 44 of the outlet header H4.
  • the refrigerants flowing out from the third lower tube Tb3 flow into the internal space 44 of the outlet header H4.
  • the refrigerants flowing from the third upper tube Ta3 into the outlet header H4 merge with the refrigerants flowing from the third lower tube Tb3 into the outlet header in the internal space 44 of the outlet header H4, and then flow into the refrigeration cycle, not illustrated, via the outlet section 32.
  • the refrigerants flowing into the inlet header H1 are in a gas-liquid mixture state in which a ratio of liquid-phase refrigerants is relatively high.
  • the liquid-phase refrigerants are higher in relative density than gas-phase refrigerants. For this reason, the liquid-phase refrigerants higher in mass tend to move downward due to an influence of gravity, as illustrated in Fig. 3 .
  • the refrigerants flowing into the intermediate header H2 are in the gas-liquid mixture state in which the ratio of the liquid-phase refrigerants decrease to be lower the ratio in the refrigerants flowing through the inlet header H1. This is because the refrigerants absorb the heat of the battery cells 21 at a time of flowing through the first upper tube Ta1 and the first lower tube Tb1 and a part of the liquid-phase refrigerants evaporate and transform into the gas-phase refrigerants. However, the refrigerants flowing into the intermediate header H2 are still in the gas-liquid mixture state. That is, the refrigerants have humidity wetness to a certain extent. For this reason, the liquid-phase refrigerants higher in mass also tend to move downward due to the influence of the gravity in the intermediate header H2, as illustrated in Fig. 3 .
  • the refrigerants flowing into the intermediate header H3 are in the gas-liquid mixture state in which the ratio of the liquid-phase refrigerants further decreases to be lower the ratio in the refrigerants flowing through the intermediate header H2. This is because the refrigerants absorb the heat of the battery cells 21 at a time of flowing through the second upper tube Ta2 and the second lower tube Tb2 and a part of the liquid-phase refrigerants evaporate and transform into the gas-phase refrigerants. However, the refrigerants flowing into the intermediate header H3 are still in the gas-liquid mixture state. That is, the refrigerants have humidity wetness to a certain extent. For this reason, the liquid-phase refrigerants higher in mass also tend to move downward due to the influence of the gravity in the intermediate header H3, as illustrated in Fig. 3 .
  • the refrigerants flowing into the outlet header H4 are in the gas-liquid mixture state in which the ratio of the liquid-phase refrigerants further decreases to be lower than the ratio in the refrigerants flowing through the intermediate header H3. This is because the refrigerants absorb the heat of the battery cells 21 at a time of flowing through the third upper tube Ta3 and the third lower tube Tb3 and a part of the liquid-phase refrigerants evaporate and transform into the gas-phase refrigerants.
  • the refrigerants flowing into the outlet header H4 are in a state in which the refrigerants hardly contain the liquid-phase refrigerants as illustrated in Fig. 3 or are in a completely gas-phase state (not illustrated). That is, the humidity wetness is nearly zero.
  • the partition member S2 is provided in the intermediate header H2 and completely partitions the upper space 42a from the lower space 42b.
  • the refrigerants flowing through above the partition member S2 among the refrigerants in the gas-liquid mixture state flowing into the intermediate header H2 do not move below the partition member S2 even if the liquid-phase refrigerants move downward in the intermediate header H2 due to the influence of the gravity.
  • the ratio of the liquid-phase refrigerants flowing through the second upper tube Ta2 that is coupled with an upper portion of the intermediate header H2 and into which the refrigerants flow from the intermediate header H2 is ensured to a certain extent. That is, an increase in the ratio of the gas-phase refrigerants is reduced.
  • the partition member S3 is provided in the intermediate header H3 and completely partitions the upper space 43a from the lower space 43b.
  • the refrigerants flowing through above the partition member S3 among the refrigerants in the gas-liquid mixture state flowing into the intermediate header H3 do not move below the partition member S3 even if the liquid-phase refrigerants move downward in the intermediate header H3 due to the influence of the gravity.
  • the ratio of the liquid-phase refrigerants flowing through the third upper tube Ta3 that is coupled with an upper portion of the intermediate header H3 and into which the refrigerants flow from the intermediate header H3 is ensured to a certain extent. That is, an increase in the ratio of the gas-phase refrigerants is reduced.
  • a cooling heat exchanger 30A according to a second embodiment will next be described with reference to the drawings.
  • the cooling heat exchanger 30A according to the second embodiment is disposed in a battery pack case 10A, and common elements to those in the cooling heat exchanger 30 according to the first embodiment are denoted by the same reference signs and will not be described in detail.
  • the cooling heat exchanger 30A cools the battery stacked bodies 20 and differs from the cooling heat exchanger 30 according to the first embodiment in that a squeeze member S1 is provided in the inlet header H1.
  • the cooling heat exchanger 30A is preferably formed by integrally bonding the four headers H, the eight heat exchange tubes T, the inlet section 31, the outlet section 32, the partition members S2 and S3, and the squeeze member S1 by brazing. High rigidity of the cooling heat exchanger 30A can be thereby ensured.
  • An interior of the inlet header H1 is partitioned into an upper space 41a and a lower space 41b by the squeeze member S1.
  • a squeeze hole S1a is formed in the squeeze member S1.
  • An area of the squeeze hole S1a is smaller than a cross-sectional area of the internal space along a direction orthogonal to the longitudinal direction of the inlet header H1.
  • the interior of the inlet header H1 is partitioned into the upper space 41a and the lower space 41b, while the squeeze hole S1a brings the upper space 41a into communication with the lower space 41b.
  • the first upper tube Ta1 communicates the upper space 41a of the inlet header H1 with the upper space 42a of the intermediate header H2.
  • the first lower tube Tb1 communicates the lower space 41b of the inlet header H1 with the lower space 42b of the intermediate header H2.
  • the inlet section 31 has the cylindrical flange portion provided in the metal tube and inserted into the hole portion formed in the inlet header H1. The downstream end of the inlet section 31 opens to the upper space 41a of the inlet header H1.
  • the inlet section 31 is attached to the inlet header H1 at a position above the squeeze member S1.
  • the gas-liquid mixture refrigerants flowing through the inlet section 31 flow into the upper space 41a of the inlet header H1.
  • the liquid-phase refrigerants relatively high in relative density move downward of the upper space 41a due to the influence of the gravity and gather near the squeeze member S1.
  • a part of the refrigerants arriving at the squeeze member S1 pass through the squeeze hole S1a and move into the lower space 41b.
  • the refrigerants that do not pass through the squeeze hole S1a flow into the first upper tube Ta1.
  • the refrigerants flowing into the upper space 41a are discharged by passing through either the first upper tube Ta1 or the squeeze hole S1a.
  • a passage resistance of a path passing through the upper tubes Ta1, Ta2, and Ta3 relatively decreases with respect to a passage resistance of a path passing through the lower tubes Tb1, Tb2, and Tb3 (passage resistance of the lower tubes) by providing the squeeze member S1. For this reason, a ratio of the refrigerants passing through the upper tubes Ta1, Ta2, and Ta3 can be increased.
  • the present invention is not limited to the first and second embodiments as long as operations and effects of the present invention can be exhibited.
  • the number of intermediate headers is two, the number of intermediate headers may be one or may be three or more.
  • the refrigerants passing through the second upper tube Ta2 and the second lower tube Tb2 directly flow into the outlet header (H4).
  • the number of intermediate headers is two or more, the refrigerants passing through the second upper tube Ta2 and the second lower tube Tb2 indirectly flow into the outlet header(H4).
  • the cooling heat exchanger includes two or more intermediate headers
  • partition members are provided in all the intermediate headers.
  • the cooling heat exchanger of the present invention include the other aspect.
  • the cooling heat exchanger including the two intermediate headers is preferably configured such that the partition member S2 is provided in the most upstream intermediate header H2.
  • the refrigerants flowing into the most upstream intermediate header H2 among the plurality of intermediate headers are higher in the ratio of the liquid-phase refrigerants than the refrigerants flowing into the intermediate header H3 disposed downstream, and the liquid-phase refrigerants tend to move downward due to the influence of the gravity.
  • the partition member S2 in the most upstream intermediate header H2 it is possible to effectively prevent the reduction in the ratio of the liquid-phase refrigerants flowing into the second upper tube Ta2.
  • each squeeze hole S1a may be provided in the squeeze member S1.
  • a shape of each squeeze hole S1a is selected from among a circular shape, an elliptical shape, and the like, as appropriate.
  • each of cooling heat exchangers 30, 30A, and 30B is not limited to an aspect such that the headers H stand upright.
  • the cooling heat exchanger 30B may be entirely disposed inclined toward the battery stacked bodies 20 while the upper tubes Ta are located above the lower tubes Tb. Reference is made to Fig. 5 .
  • the cooling heat exchanger 30B stands in such a manner that an extension axis HX of the headers H has an angle ⁇ with respect to a bottom surface 10a of the battery pack case 10.
  • the upper tubes Ta and the lower tubes Tb come in surface contact with the soaking layers 22 of the battery stacked bodies 20.
  • the elements are preferably assembled into the cooling heat exchanger 30B at the angle ⁇ in a range from 70 degrees to 110 degrees in light of shapes of the battery stacked bodies 20 and the effects of the present invention.
  • a battery cooling device is suited for being mounted in an electric-powered vehicle or a hybrid vehicle.

Landscapes

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Secondary Cells (AREA)
EP21741235.2A 2020-01-17 2021-01-13 Échangeur de chaleur de refroidissement Pending EP4092813A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2020006054 2020-01-17
PCT/JP2021/000741 WO2021145317A1 (fr) 2020-01-17 2021-01-13 Échangeur de chaleur de refroidissement

Publications (1)

Publication Number Publication Date
EP4092813A1 true EP4092813A1 (fr) 2022-11-23

Family

ID=76863869

Family Applications (1)

Application Number Title Priority Date Filing Date
EP21741235.2A Pending EP4092813A1 (fr) 2020-01-17 2021-01-13 Échangeur de chaleur de refroidissement

Country Status (4)

Country Link
EP (1) EP4092813A1 (fr)
JP (1) JPWO2021145317A1 (fr)
CN (1) CN114830412A (fr)
WO (1) WO2021145317A1 (fr)

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011049139A (ja) * 2009-07-31 2011-03-10 Sanyo Electric Co Ltd バッテリー装置
JP2012190675A (ja) * 2011-03-11 2012-10-04 Sanyo Electric Co Ltd バッテリー装置
JP6295580B2 (ja) 2013-10-03 2018-03-20 日産自動車株式会社 バッテリ温調装置
FR3024537B1 (fr) 2014-08-04 2019-03-22 Valeo Systemes Thermiques Echangeur thermique et dispositif de gestion thermique correspondant

Also Published As

Publication number Publication date
JPWO2021145317A1 (fr) 2021-07-22
WO2021145317A1 (fr) 2021-07-22
CN114830412A (zh) 2022-07-29

Similar Documents

Publication Publication Date Title
US10996002B2 (en) Evaporator
JP6004402B2 (ja) 電池セル冷却器、装置、および方法
CN108242520B (zh) 车辆电池保持结构
US9989315B2 (en) Cold storage heat exchanger
US20170341483A1 (en) Battery temperature control device and battery temperature control system
CN102778083B (zh) 冷却储存式热交换器
CN112219308A (zh) 用于冷却至少一个机动车辆电池的系统
JP6183100B2 (ja) 蓄冷熱交換器
US9581369B2 (en) Evaporator with phase change material
US20140090812A1 (en) Heat exchanger
US9666894B2 (en) Battery module and method for manufacturing the same
EP3059542B1 (fr) Collecteur stratifié, échangeur de chaleur, et climatiseur
JP5920087B2 (ja) 蓄冷熱交換器
JP2011133126A (ja) 蓄冷機能付きエバポレータ
EP4092813A1 (fr) Échangeur de chaleur de refroidissement
US10696128B2 (en) Cold storage heat exchanger
JP2021131199A (ja) 冷却用熱交換器
KR101170610B1 (ko) 축냉 열교환기
JP2010243066A (ja) 蓄冷熱交換器
US8893521B2 (en) Multi-cooling module for vehicle
CN214469458U (zh) 微通道平行流换热器
JP2021174662A (ja) 車両用バッテリ冷却装置の熱交換器
JP6919511B2 (ja) 蒸発器
CN111919332A (zh) 用于机动车辆电池单元的冷却系统
JP7077763B2 (ja) 機器温調装置

Legal Events

Date Code Title Description
STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE INTERNATIONAL PUBLICATION HAS BEEN MADE

PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE

17P Request for examination filed

Effective date: 20220713

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

DAV Request for validation of the european patent (deleted)
DAX Request for extension of the european patent (deleted)
P01 Opt-out of the competence of the unified patent court (upc) registered

Effective date: 20230629